Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L27/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
  • C08L27/02—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L27/12—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L27/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
  • C08L27/02—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L27/12—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
  • C08L27/18—Homopolymers or copolymers or tetrafluoroethene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L71/00—Compositions of polyethers obtained by reactions forming an ether link in the main chain; Compositions of derivatives of such polymers
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
  • Y10T428/00—Stock material or miscellaneous articles
  • Y10T428/13—Hollow or container type article [e.g., tube, vase, etc.]
  • Y10T428/1352—Polymer or resin containing [i.e., natural or synthetic]
  • Y10T428/139—Open-ended, self-supporting conduit, cylinder, or tube-type article
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
  • Y10T428/00—Stock material or miscellaneous articles
  • Y10T428/31504—Composite [nonstructural laminate]
  • Y10T428/3154—Of fluorinated addition polymer from unsaturated monomers

Definitions

• This invention relates to blends of fluoroplastics and polyetherketoneketone having improved properties.
• Fluoroplastics which are fabricable by melt flow at temperatures above their melting points have a wide range of utilities because of their chemical inertness and high melting temperature. These utilities could be broadened if such properties as room temperature toughness, high temperature physical properties such as heat distortion temperature and/or permeability could be improved.
• the use of additives in the fluoroplastic in an attempt to achieve such improvement suffers from one or more problems of incompatibility with the fluoroplastic, resulting in deterioration of desired properties, and difficulty in uniformly incorporating the additive into the fluoroplastic.
• the present invention is a composition comprising 5 to 95 wt% melt-flowable fluoroplastic and complementally, to total 100 wt%, 95 to 5 wt% PEKK.
• the melt-flowability of the fluoroplastic enables it to be fabricated by melt extrusion, including injection molding.
• the fluoroplastic can have a melt flow rate (MFR) in the range of 1 to 100 g/10 min determined in accordance with ASTM D- 1238 at the temperature which is standard for the fluoroplastic.
• MFR melt flow rate
• the fluoroplastic is non-elastomeric, i.e. the stress-strain curve for the fluoroplastic exhibits a yield point, and upon further stretching of the fluoroplastic, there is little recovery of strain (stretch), e.g. less than 20%, upon release of the stretching force.
• melt-fabricable fluoroplastics include the group of well known fluoropolymers comprising tetrafluoroethylene (TFE) copolymers, particularly the copolymers of TFE with one or more comonomers selected from perfluoroolefins having 3-8 carbon atoms, preferably hexafluoropropylene (HFP), and perfluoro(alkyl vinyl ether) (PAVE) with alkyl groups having 1-5 carbon atoms, preferably 1-3 carbon atoms, most preferably 2-3 carbon atoms.
• TFE tetrafluoroethylene
• HFP hexafluoropropylene
• PAVE perfluoro(alkyl vinyl ether)
• Such copolymers have sufficient concentration of comonomer to reduce the melting temperature of the copolymer significantly below that of TFE homopolymer.
• TFE/HFP typically referred to as FEP
• TFE/PAVE typically referred to as PFA
• TFE/HFP/PAVE TFE/HFP/PAVE.
• the aforesaid TFE copolymers can also contain minor amounts of units derived from other comonomers, including polar-functional monomers that introduce polar groups along the polymer chain, usually at the end of pendant side groups, when copolymerized into the polymer.
• Fluoroplastics other than the perfluorinated copolymers mentioned above can also be used, such as copolymers of TFE or chlorotrifluoroethylene (CTFE) with ethylene, and TFE/HFP/vinylidene fluoride copolymer (THV).
• CTFE chlorotrifluoroethylene
• TFE/HFP/vinylidene fluoride copolymer TFE/HFP/vinylidene fluoride copolymer
• the processing of the fluoroplastic at temperature above its melting point indicates that the fluoroplastic has crystallinity.
• the fluoroplastic used in the present invention may also be amorphous, however, in which case, the processing of the fluoroplastic is at a high temperature that the PEKK will be flowable as though molten during the processing.
• a portion of the melt-fabricable fluoroplastic is replaced by polytetrafluoroethylene (PTFE) micropowder.
• PTFE micropowder is a tetrafluoroethylene homopolymer or modified homopolymer which has a considerably lower molecular weight than the normal high melt viscosity PTFE, which enables the micropowder by itself to be melt flowable, having a melt flow rate within the range described for the melt-fabricable fluoroplastics.
• the high molecular weight of the normal PTFE is characterized by a molecular weight (Mn) of at least 2,000,000 and a melt viscosity of at least 10 8 Pa.s at 380°C, this melt viscosity being so high that the PTFE does not flow in the molten state, requiring special non-melt-fabrication techniques, including paste extrusion for the fine powder type of PTFE and compression molding for the granular type of PTFE.
• the molecular weight (Mn) of PTFE micropowder will usually be within the range of 50,000 to 700,000, and the melt viscosity of the micropowder will be 50 to 1 X 10 5 Pa ⁇ s as measured at 372°C in accordance with the procedure of ASTM D-1239-52T, modified as disclosed in U.S. Patent 4,380,618.
• the melt viscosity of the PTFE micropowder is 100 to 1 X 10 4 Pa ⁇ s at 372°C.
• PTFE micropowder is described further in Kirk-Othmer, The Encyclopedia of Chemical Technology, 4 th Ed., pub. by John Wiley & Sons (1994) on pp 637-639 of Vol.
• melt-fabricable fluoroplastic When a portion of the melt-fabricable fluoroplastic is replaced by PTFE micropwder, at least 10% by weight of the total fluoroplastic will be the melt-fabricable fluoroplastic, preferably at least 20 wt%, the remainder being the PTFE micropowder.
• the PTFE micropowder imparts increased strength to articles molded from the fluoroplastic/PEKK blend, even though the PTFE micropowder has no strength by itself as described above.
• the PEKK component is a copolymer of diphenyl ether and benzene dicarboxylic acid halides, preferably terephthalyl (T) or isophthaloyl (I) halides, usually chlorides, and mixtures thereof, such as disclosed in U.S. Patents 3,062,205, 3,441,538, 3,442,857, 3,516,966, 4,704,448, and 4,816,556, preferably having an inherent viscosity of at least 0.4 measured on a 0.5 wt% solution in concentrated sulfuric acid at 30°C.
• the PEKK generally has a melting point of at least 300°C.
• the PEKK contains both T and I units in a ratio of 90:10 to 30:70, and more typically 80:20 to 60:40. As the proportion of T units decrease and I units increase, the crystallinity of the PEKK diminishes, until at 60:40, the PEKK crystallizes so slowly that it resembles an amorphous polymer, except that it will exhibit a melting point.
• the preferred composition has at least 25 wt% of the melt-flowable fluoroplastic.
• the proportion of the fluoroplastic will vary.
• One of the improvements which a relatively small amount of PEKK imparts to the fluoroplastic is improved cut-through resistance which is especially valuable in the use of fluoroplastic for insulation coating or jacketing of insulated wire.
• the PEKK content of the composition will be 5 to 25 wt%, preferably 10 to 20 wt%.
• the PEKK is incompatible with the fluoroplastic as indicated by the PEKK being present as discrete particles (domains) dispersed in the fluoroplastic matrix forming the insulation or jacketing, the electrical properties and tensile elongation of the insulation and jacketing does not suffer.
• PEKK polystyrene-maleic anhydride copolymer
• high temperature resistance to distortion under load is especially valuable for applications in which the fluoroplastic forms a structural member, such as baskets for carrying articles through exposure to chemical processing at high temperatures.
• fluoroplastics tend to creep and distort at temperatures as low as 60 to 100°C.
• PEKK imparts much greater resistance to creep and distortion at elevated temperatures than would be expected from the amount of PEKK used. This greater resistance to creep and distortion can be measured as increased heat distortion temperature in accordance with ASTM D648 using 264 psi (1816 MPa) load.
• Dispersion of PEKK in fluoroplastic can provide blends which have heat distortion temperatures (HDT) greater than 100°C., and even greater than 140°C, enabling the fluoroplastic to have a higher service temperature, without detracting from the chemical inertness of the fluoroplastic.
• the PEKK content of the composition can be 5 to 30 wt%, preferably 10 to 30 wt%, and more preferably 15 to 25 wt%.
• the resultant composition exhibits remarkable creep resistance, i.e. resistance to cold flow.
• the composition has physical integrity, so as to be useful in structural applications providing the improved performance of dimensional integrity. This embodiment is demonstrated is especially valuable in pipe lining.
• the incorporation of dispersed fluoroplastic therein provides for improved impermeability to organic fluid and improved toughness.
• Fluoroplastic by itself has high impermeability to such hydrocarbon fluids as fuel as compared to the relatively high permeability of PEKK to such fluid.
• coextruded tubing of a fluoroplastic inner layer and a layer of the blend (dispersion of the fluoroplastic in the PEKK) of the present invention is highly useful in applications for transporting such hydrocarbon fluid as fuel both on board motorized vehicles and in stationary applications.
• the fluoroplastic and PEKK components can be melt blended as part of the extrusion process or can be premixed, followed by melt blending at temperature at which both resins are molten. Generally, the melt blending temperature will be at least 300°C. Under this condition, the PEKK or the fluoroplastic, as the case may be, becomes uniformly dispersed as fine particles (domains) in the component which becomes the matrix.
• the resultant extrudate can be the final molded article, such as in the case of an injection molded article or an extruded tube, sheet or coating, or can be chopped into molding granules for subsequent melt processing into the article desired.
• compositions of the present invention can contain other ingredients such as pigments for coloring the composition or fillers, such as mica, glass, carbon, or aramid, in fibrous or other particulate form.
• the PEKK aids in dispersing the filler in the fluoroplastic matrix. When filler is present, the amount present will be 0.5 to 30 wt% based on the combined weight of PEKK, fluoroplastic and filler.
• the general procedure for melt blending to form blends of the present invention as described in the following Examples was as follows: The fluoroplastic and PEKK were fed in the proportions desired to a twin-screw extruder equipped with high shear screws for melt blending under vaccuum to remove any gas that may be generated. The maximum extruder temperature is reported in the Examples. The resulting melt blend was extruded as strands, cooled and chopped up into pellets for injection and compression molding at temperatures of 330 to 370°C for testing. The melt flow rates (MFR) disclosed in the Examples are typical for the respective fluoropolymers as indicated in the commercial product literature. The PEKK used in the Examples is made by the process disclosed in U.S. patent 4,816,556 (Gay et al.)
• the fluoroplastic was TEFLON® PFA fluoropolymer resin grade 350 (MFR 2g/10 min at 372°C) and the PEKK contained T and I units in a 80/20 ratio.
• the extruder temperature used was 360°C.
• Blends containing 5 to 30 wt% of the fluoroplastic dispersed in the PEKK matrix were made and tested for high temperature distortion (test previously described) and tensile modulus, with the results shown in the following tables:
• Blends were made in which the PEKK contained T and I units in a 60/40 ratio was the PFA was the 340 grade.
• the PEKK contained about 10 wt% of TiO 2 filler, based on the weight of the PEKK plus filler, and the PEKK/filler blend constituted 70 to 80 wt% of the total composition.
• the temperature of the twin screw extruder was 370°C.
• the 80 wt% composition was tested for tensile modulus, which was 471 ksi (3250 MPa) as compared to 495 ksi (3416 MPa) for the PEKK composition by itself and 64 ksi (442 MPa) for the PFA by itself.
• the incorporation of the PFA into the PEKK resulted in an unexpectedly small reduction in the tensile modulus of the PEKK composition, while imparting improved chemical resistance to the overall composition.
• the PEKK composition of Example 2 was used and the fluoroplastic was TFE/HFP copolymer (TEFLON® FEP fluoropolymer resin grade 100, MFR 7 g/10 min at 372°). Blends containing 5 to 30 wt% of this fluoroplastic and 95 to 70 wt% of the PEKK were prepared using a twin screw extruder operating at 370°C.
• the tensile modulus of the FEP by itself is 50 ksi (345 MPa).
• the tensile moduli of the blends having 5, 10 and 20 wt% of the FEP were determined and all were greater than 436 ksi (3008 MPa) obtained for the 20 wt% blend, which is unexpectedly high.
• a blend of 80 wt% TEFZEL® ETFE fluoropolymer grade 280 (MFR 4g/10 min at 297°C) and 20 wt% of the PEKK used in Example 1 was prepared in the twin screw extruder at a temperature of 370°C and tested for tensile modulus.
• the TEFZEL fluoroplastic by itself exhibited a tensile modulus of 186 ksi (1283 MPa), and the blend exhibited a tensile modulus of 263 ksi (1815 MPa), which is greater than the increase that would have been expected from the tensile modulus of the PEKK.
• a similar result was obtained when the PEKK of Example 2 was used; the 80/20 blend exhibited a tensile modulus of 260 ksi (1794 MPa).
• This Example shows the unexpectedly high tensile modulus of blends of fluoroplastic and PEKK when the fluoroplastic is a combination of melt-fabricable and melt-flowable, not melt-fabricable fluoroplastics.
• the PEKK used was that of Example 1, tensile modulus of 530 ksi
• the melt-fabricable fluoroplastic was TEFLON® PFA fluoropolymer grade 440HP (MFR 13 g/10 min at 372°) exhibiting a tensile modulus of 80 ksi (552 MPa)
• the melt flowable, not melt-fabricable fluoroplastic (PTFE micropowder) was ZONYL® fluoroadditive grade MP 1600 (MFR 17 g/10 min at 372°C) exhibiting no tensile strength (zero tensile modulus), because the tensile test bars break upon clamping in the tensile testing machine.
• Table 3 shows that even only a small proportion of PEKK doubles the tensile modulus of the PFA considered by itself, and that the MP 1600 fluoroadditive which has no tensile modulus, does not detract from the tensile strengthening of the blend.
• the MP 1600 fluoroadditive which has no tensile strength, can constitute a substantial proportion of the blend with PEKK, wherein the blend has high tensile modulus.
• This provides a utility for the MP1600 fluoroadditive in molded articles, in contrast to prior utilities for this fluoropolymers as a particulate solid lubricant in liquid media or as a component in a supported coating composition.
• the PTFE micropowder also imparts improved chemical resistance and lubricity to the blend.
• This Example shows the improved creep resistance (reduced creep) of blends of the present invention.
• the fluoropolymer used was the PFA of Example 1 and the PEKK used was that of Example 1.
• the creep of test specimens of the blends was measured by DMA (Dynamic Mechanical Analyzer) at 100°C using a 500 g load. The creep is the increase in length of the specimen as a percent of the original length (% elongation)
• Table 3 shows that as little as 5 wt% PEKK reduces the initial elongation by 19% and the long term elongation (creep) by 21%. The presence of 20 wt% PEKK in the blend decreases creep by almost 400%.

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• Organic Chemistry (AREA)
• Compositions Of Macromolecular Compounds (AREA)

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• 1998
  • 1998-06-15 US US09/094,942 patent/US6177518B1/en not_active Expired - Lifetime
  • 1998-06-22 DE DE1998617708 patent/DE69817708T2/de not_active Expired - Lifetime
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